EP3059007A1 - Stirrer for stirring molten glass, apparatus for stirring molten glass comprising such a stirrer and use of such a stirrer - Google Patents
Stirrer for stirring molten glass, apparatus for stirring molten glass comprising such a stirrer and use of such a stirrer Download PDFInfo
- Publication number
- EP3059007A1 EP3059007A1 EP15156128.9A EP15156128A EP3059007A1 EP 3059007 A1 EP3059007 A1 EP 3059007A1 EP 15156128 A EP15156128 A EP 15156128A EP 3059007 A1 EP3059007 A1 EP 3059007A1
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- EP
- European Patent Office
- Prior art keywords
- stirrer
- blades
- blade
- stirrer blades
- normal vector
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
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Classifications
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- C—CHEMISTRY; METALLURGY
- C03—GLASS; MINERAL OR SLAG WOOL
- C03B—MANUFACTURE, SHAPING, OR SUPPLEMENTARY PROCESSES
- C03B5/00—Melting in furnaces; Furnaces so far as specially adapted for glass manufacture
- C03B5/16—Special features of the melting process; Auxiliary means specially adapted for glass-melting furnaces
- C03B5/18—Stirring devices; Homogenisation
- C03B5/187—Stirring devices; Homogenisation with moving elements
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- C—CHEMISTRY; METALLURGY
- C03—GLASS; MINERAL OR SLAG WOOL
- C03B—MANUFACTURE, SHAPING, OR SUPPLEMENTARY PROCESSES
- C03B5/00—Melting in furnaces; Furnaces so far as specially adapted for glass manufacture
- C03B5/16—Special features of the melting process; Auxiliary means specially adapted for glass-melting furnaces
- C03B5/18—Stirring devices; Homogenisation
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F27/00—Mixers with rotary stirring devices in fixed receptacles; Kneaders
- B01F27/05—Stirrers
- B01F27/051—Stirrers characterised by their elements, materials or mechanical properties
- B01F27/053—Stirrers characterised by their elements, materials or mechanical properties characterised by their materials
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F27/00—Mixers with rotary stirring devices in fixed receptacles; Kneaders
- B01F27/05—Stirrers
- B01F27/07—Stirrers characterised by their mounting on the shaft
- B01F27/071—Fixing of the stirrer to the shaft
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F27/00—Mixers with rotary stirring devices in fixed receptacles; Kneaders
- B01F27/05—Stirrers
- B01F27/07—Stirrers characterised by their mounting on the shaft
- B01F27/072—Stirrers characterised by their mounting on the shaft characterised by the disposition of the stirrers with respect to the rotating axis
- B01F27/0723—Stirrers characterised by their mounting on the shaft characterised by the disposition of the stirrers with respect to the rotating axis oblique with respect to the rotating axis
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F27/00—Mixers with rotary stirring devices in fixed receptacles; Kneaders
- B01F27/05—Stirrers
- B01F27/07—Stirrers characterised by their mounting on the shaft
- B01F27/072—Stirrers characterised by their mounting on the shaft characterised by the disposition of the stirrers with respect to the rotating axis
- B01F27/0724—Stirrers characterised by their mounting on the shaft characterised by the disposition of the stirrers with respect to the rotating axis directly mounted on the rotating axis
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F27/00—Mixers with rotary stirring devices in fixed receptacles; Kneaders
- B01F27/05—Stirrers
- B01F27/07—Stirrers characterised by their mounting on the shaft
- B01F27/072—Stirrers characterised by their mounting on the shaft characterised by the disposition of the stirrers with respect to the rotating axis
- B01F27/0727—Stirrers characterised by their mounting on the shaft characterised by the disposition of the stirrers with respect to the rotating axis having stirring elements connected to the stirrer shaft each by two or more radial rods, e.g. the shaft being interrupted between the rods, or of crankshaft type
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F27/00—Mixers with rotary stirring devices in fixed receptacles; Kneaders
- B01F27/05—Stirrers
- B01F27/07—Stirrers characterised by their mounting on the shaft
- B01F27/074—Stirrers characterised by their mounting on the shaft having two or more mixing elements being concentrically mounted on the same shaft
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F27/00—Mixers with rotary stirring devices in fixed receptacles; Kneaders
- B01F27/05—Stirrers
- B01F27/11—Stirrers characterised by the configuration of the stirrers
- B01F27/112—Stirrers characterised by the configuration of the stirrers with arms, paddles, vanes or blades
- B01F27/1125—Stirrers characterised by the configuration of the stirrers with arms, paddles, vanes or blades with vanes or blades extending parallel or oblique to the stirrer axis
- B01F27/11253—Stirrers characterised by the configuration of the stirrers with arms, paddles, vanes or blades with vanes or blades extending parallel or oblique to the stirrer axis the blades extending oblique to the stirrer axis
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F27/00—Mixers with rotary stirring devices in fixed receptacles; Kneaders
- B01F27/05—Stirrers
- B01F27/11—Stirrers characterised by the configuration of the stirrers
- B01F27/114—Helically shaped stirrers, i.e. stirrers comprising a helically shaped band or helically shaped band sections
- B01F27/1144—Helically shaped stirrers, i.e. stirrers comprising a helically shaped band or helically shaped band sections with a plurality of blades following a helical path on a shaft or a blade support
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F27/00—Mixers with rotary stirring devices in fixed receptacles; Kneaders
- B01F27/05—Stirrers
- B01F27/11—Stirrers characterised by the configuration of the stirrers
- B01F27/114—Helically shaped stirrers, i.e. stirrers comprising a helically shaped band or helically shaped band sections
- B01F27/1145—Helically shaped stirrers, i.e. stirrers comprising a helically shaped band or helically shaped band sections ribbon shaped with an open space between the helical ribbon flight and the rotating axis
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F27/00—Mixers with rotary stirring devices in fixed receptacles; Kneaders
- B01F27/05—Stirrers
- B01F27/11—Stirrers characterised by the configuration of the stirrers
- B01F27/19—Stirrers with two or more mixing elements mounted in sequence on the same axis
- B01F27/192—Stirrers with two or more mixing elements mounted in sequence on the same axis with dissimilar elements
- B01F27/1921—Stirrers with two or more mixing elements mounted in sequence on the same axis with dissimilar elements comprising helical elements and paddles
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F27/00—Mixers with rotary stirring devices in fixed receptacles; Kneaders
- B01F27/23—Mixers with rotary stirring devices in fixed receptacles; Kneaders characterised by the orientation or disposition of the rotor axis
- B01F27/231—Mixers with rotary stirring devices in fixed receptacles; Kneaders characterised by the orientation or disposition of the rotor axis with a variable orientation during mixing operation, e.g. with tiltable rotor axis
- B01F27/2312—Mixers with rotary stirring devices in fixed receptacles; Kneaders characterised by the orientation or disposition of the rotor axis with a variable orientation during mixing operation, e.g. with tiltable rotor axis the position of the rotating shaft being adjustable in the interior of the receptacle, e.g. to locate the stirrer in different locations during the mixing
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F27/00—Mixers with rotary stirring devices in fixed receptacles; Kneaders
- B01F27/50—Pipe mixers, i.e. mixers wherein the materials to be mixed flow continuously through pipes, e.g. column mixers
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- C—CHEMISTRY; METALLURGY
- C03—GLASS; MINERAL OR SLAG WOOL
- C03B—MANUFACTURE, SHAPING, OR SUPPLEMENTARY PROCESSES
- C03B5/00—Melting in furnaces; Furnaces so far as specially adapted for glass manufacture
- C03B5/16—Special features of the melting process; Auxiliary means specially adapted for glass-melting furnaces
- C03B5/167—Means for preventing damage to equipment, e.g. by molten glass, hot gases, batches
- C03B5/1672—Use of materials therefor
-
- C—CHEMISTRY; METALLURGY
- C03—GLASS; MINERAL OR SLAG WOOL
- C03B—MANUFACTURE, SHAPING, OR SUPPLEMENTARY PROCESSES
- C03B5/00—Melting in furnaces; Furnaces so far as specially adapted for glass manufacture
- C03B5/16—Special features of the melting process; Auxiliary means specially adapted for glass-melting furnaces
- C03B5/167—Means for preventing damage to equipment, e.g. by molten glass, hot gases, batches
- C03B5/1672—Use of materials therefor
- C03B5/1675—Platinum group metals
-
- C—CHEMISTRY; METALLURGY
- C03—GLASS; MINERAL OR SLAG WOOL
- C03B—MANUFACTURE, SHAPING, OR SUPPLEMENTARY PROCESSES
- C03B5/00—Melting in furnaces; Furnaces so far as specially adapted for glass manufacture
- C03B5/16—Special features of the melting process; Auxiliary means specially adapted for glass-melting furnaces
- C03B5/18—Stirring devices; Homogenisation
- C03B5/187—Stirring devices; Homogenisation with moving elements
- C03B5/1875—Stirring devices; Homogenisation with moving elements of the screw or pump-action type
-
- C—CHEMISTRY; METALLURGY
- C03—GLASS; MINERAL OR SLAG WOOL
- C03B—MANUFACTURE, SHAPING, OR SUPPLEMENTARY PROCESSES
- C03B7/00—Distributors for the molten glass; Means for taking-off charges of molten glass; Producing the gob, e.g. controlling the gob shape, weight or delivery tact
- C03B7/08—Feeder spouts, e.g. gob feeders
- C03B7/086—Plunger mechanisms
-
- C—CHEMISTRY; METALLURGY
- C03—GLASS; MINERAL OR SLAG WOOL
- C03B—MANUFACTURE, SHAPING, OR SUPPLEMENTARY PROCESSES
- C03B7/00—Distributors for the molten glass; Means for taking-off charges of molten glass; Producing the gob, e.g. controlling the gob shape, weight or delivery tact
- C03B7/08—Feeder spouts, e.g. gob feeders
- C03B7/092—Stirring devices; Homogenisation
Definitions
- the invention concerns a stirrer for stirring molten glass, and apparatus for stirring molten glass which comprises such a stirrer and the use of such a stirrer for homogenizing molten glass.
- melt process of the constituents alone may leave inhomogeneities, which can present itself as discolorations or as sections with a different refractive index.
- Such a stirring apparatus essentially consists of a stirring chamber in which a stirrer is placed.
- Such stirring apparatuses may work in a continuous process, or may be batch apparatuses, treating one batch of molten glass at a time.
- stirrers for molten glass are usually made of platinum or a platinum-based alloy, because this is the one of the few materials having sufficient mechanical strength and chemical inertness at the temperatures needed for melting glass. As the platinum price is very high, an important further consideration when designing stirrers for molten glass is to limit the amount of material needed.
- An alternative material that may be used, especially in less demanding glass stirring applications, is molybdenum or a molybdenum-based alloy, which may or may not be clad with platinum.
- stirrer should have no significant pumping function, as changes in the rotational speed will then cause changes in the pressure drop over the molten glass supply system, which will in turn create variations in the properties of glass products formed at the end of the molten glass supply system, eg sheets of display glass.
- stirrers for molten glass having no or only limited pumping effect are given in DE102008017045 , WO2011020625 and US8434329 .
- Their stirrer blades are disposed parallel to the direction in which the stirrers are rotating or at right angles to this direction, meaning that either there is mainly cutting of stirrer blades through the molten glass leading to a chopping effect on inhomogeneities without much elongation of non-homogenous section and redistribution of inhomogeneities, or mainly horizontal movement of the molten glass and possible elongation of inhomogeneities, without significant chopping effect, so that the homogenization performance of these stirrers is not optimal.
- the angular component of the normal vector ensures that in use both a horizontal as well as a vertical force is exercised on the molten glass, leading to a good homogenization performance.
- attached can mean either directly attached, or indirectly attached by means of another structural element of the stirrer.
- the specified angular component of the specified normal vector of a given stirrer blade may be considered to be positive or negative. This is not relevant for the definition of the invention as the direction of the stirrer blades in this invention is only considered in relation to each other.
- a rapid mixing of molten glass from the inlet zone into the bulk of the molten glass in the stirred volume can be obtained, or avoided if so desired, thereby obtaining more or less mixing, as desired, with material having entered the stirring chamber earlier, so obtaining a good smoothing out of time-dependent composition variations.
- the pumping effect can be better controlled, to be either absent, or to be more constant over a range of rotational speeds, while maintaining a placement of the individual stirrer blades which is optimal for homogenization, thereby again increasing the options for a stirrer designer to obtain a desired performance depending on the detailed requirements of a particular homogenization task.
- the one or more outer stirrer blades are mounted on rods or tubes extending at least partially in a radial direction from the shaft from the shaft, whereby the one or more outer stirrer blades each have two ends, whereby each of these ends is mounted on a different one of said rods or tubes, whereby the rods or tubes used for mounting the ends of an specific outer stirrer blade have a different angular position and/or axial position on the shaft.
- rods or tubes may have any cross-sectional shape, such as, but not limited to, round, square, elliptical.
- the outer edge of at least one of the one or more outer stirrer blades is provided with a raised edge, whereby preferably all of the mentioned outer stirrer blades are provided with such an edge.
- the angular component of the normal vector of at least a blade section in other words the entire blade or a part of a blade, of one or more of said inner and outer stirrer blades is negative and the angular component of the normal vector of at least a blade section of one or more of the inner and outer stirrer blades is positive.
- the stirrer comprises two or more of said inner stirrer blades, whereby the angular component of the normal vector of at least one of said inner stirrer blades is negative and the angular component of the normal vector of at least one other of said inner stirrer blades is positive and whereby the number and size of said inner stirrer blades having a normal vector with a negative angular component is the same as the number and size of said inner stirrer blades having a normal vector with a positive angular component.
- the one or more outer stirrer blades in totality comprise two or more blade sections, whereby the angular component of the normal vector of at least one of said blade sections is negative and the angular component of the normal vector of at least one other of said blade sections is positive and whereby the number and size of said blade sections having a normal vector with a negative angular component is the same as the number and size of said blade sections having a normal vector with a positive angular component.
- At least a blade section of one of said one or more outer stirrer blades extends over a certain axial section of the stirrer, whereby at least one of said one or more inner stirrer blades is placed in the same axial section, whereby the signs of the angular components of the normal vectors of this inner stirrer blade and this blade section of the outer stirrer blade are opposite.
- the angular component of the normal vector of an outer or inner stirrer blade on the side directed towards the tip can be a single value or can have only a single sign over the entire outer or inner stirrer blade.
- an inner or outer stirrer blade only has one single blade section, so that in this case the term blade section of an outer stirrer blade is equivalent to the outer stirrer blade and the term blade section of an inner stirrer blade is equivalent to the inner stirrer blade.
- the invention further concerns an apparatus for stirring molten glass comprising a stirring chamber and having a stirrer according to any one of the previous claims which is mounted in the stirring chamber whereby the stirrer is rotatable around the central axis of the stirrer.
- the stirrer 1 shown in figures 1 to 5 consists mainly of a shaft 2, which is provided at one extreme with a connector 3 for connecting the shaft 2 to a drive, and nearer to the other extreme, further to be called the tip 4, with a number of stirrer blades.
- the shaft 2 has a central longitudinal axis L which during use will be the axis of rotation of the stirrer 1.
- the stirrer blades can be grouped in two groups, more specifically inner stirrer blades 5,6, which are attached directly against the shaft 2 and which are helicoidally shaped, meaning shaped like a part of a helicoid, and outer stirrer blades 7, 8 which are attached to rods 9 which are attached to the shaft 2.
- the outer stirrer blades 7,8 are flat blades which are mounted on the shaft 2 according to the intersection of a plane and a cylinder, and which have a raised edge 10 at their outermost edge.
- the inner stirrer blades 5,6 make 3 ⁇ 4 turns round the shaft 2 and the outer stirrer blades 7,8 make 1 ⁇ 4 turn around the shaft 2.
- the raised edged 10 is present both above as well as below the main body of the outer stirrer blades 7,8.
- This raised edge 10 serves to reinforce the outer stirrer blades 7,8, but also has a function to improve stirrer performance, as will be explained below.
- the stirrer geometry will further be considered in a cylindrical coordinate system, similar to the cylindrical coordinate system 11 drawn in figure 1 , but with the longitudinal axial coordinate z of the cylindrical coordinate system defined to coincide with the central axis L and having an increasing value from the connector 3 to the tip 4, and further having a radial coordinate ⁇ and an angular coordinate ⁇ , defined to have an increasing value in clockwise direction when looking from the connector 3 to the tip 4.
- the two inner stirrer blades 5 closest to the tip have a normal vector N on the side of the tip 4 with a negative angular component N A , so with a direction opposite to the defined direction of the angular coordinate ⁇ , meaning that if the stirrer 2 is rotated in a positive angular direction ⁇ during use, these inner stirrer blades 5 will create an axial displacement of molten glass away from the tip 4.
- the two inner stirrer blades 6 furthest away from the tip 4 have a normal vector P on the side of the tip 4 with a positive angular component P A , so with a direction coinciding with the defined direction of the angular coordinate ⁇ , meaning that if the stirrer 2 is rotated in a positive angular direction ⁇ during use, these inner stirrer blades 6 will create an axial displacement of molten glass towards the tip 4.
- the outer stirrer blades 7, 8 are placed on rods 9 which are attached to the shaft 2 at different angular and axial positions, more specifically at angular positions 90° apart, in line with the outer stirrer blades 7,8 making 1 ⁇ 4 turn around the shaft 2.
- Each outer stirrer blade 7,8 is attached at both its ends to a different rod 9, and whereby some rods 9 are attached to the ends of two outer stirrer blades 7,8, and some other rods 9 are only a attached to the end of a single outer stirrer blade 7,8.
- outer blades 7,8 are attached at or at least close to the ends of the rods 9. It is however also possible that outer blades 7,8 are attached to the rods 9 at a point between the attachment point to the shaft 2 and the free end of the rods 9.
- the outer stirrer blades 7,8 are placed on the same axial section of the shaft 2 as the inner stirrer blades 5,6.
- the four outer stirrer blades 7 closest to the tip 4 have a normal vector Q on the side of the tip 4 with a positive angular component Q A , meaning that if the stirrer 2 is rotated in a positive angular direction ⁇ during use, these outer stirrer blades 7 will create an axial displacement of molten glass towards the tip 4.
- the four outer stirrer blades 8 furthest away from the tip 4 have a normal vector R on the side of the tip with a negative angular component R A , meaning that if the stirrer is rotated in a positive angular direction ⁇ during use, these outer stirrer blades 8 will create an axial displacement of molten glass away from the tip 4.
- the shaft 2, inner and outer stirrer blades 5,6,7,8, and the rods 9 are all made of dispersion-hardened platinum.
- stirrer is simple and as follows, and as illustrated in figure 6 .
- the stirrer may be significantly smaller than the stirring chamber, which is in that case formed by the vessel in which the stirring is performed.
- stirrer may be placed in a long channel through which glass flows, whereby the channel itself forms the stirring chamber.
- the alternative stirrers shown in figures 7 to 11 differ from the stirrer shown in figure 1 by having a different number and different arrangement of inner and outer stirrer blades.
- the stirrer 1 shown in figure 7 has the same number and arrangement of inner stirrer blades 5, 6 as the stirrer of figure 1 .
- the arrangement of outer stirrer blades 8 is different, in that this stirrer has six outer stirrer blades 8, which are all positioned so that they have a normal vector R on the side of the tip 4 with a negative angular component.
- This stirrer 1 has a pumping effect, when rotated in a positive angular direction ⁇ , away from the tip 4. This pumping effect is dependent on the rotational speed of the stirrer 1 so that this stirrer 1 is mostly suitable for batch-wise processing of molten glass.
- the stirrer 1 shown in figure 8 has the same number and arrangement of inner stirrer blades 5,6 as the stirrer 1 of figures 1 and 7 .
- the arrangement of outer stirrer blades is different, in that in addition to the outer stirrer blades 8 of the stirrer 1 of figure 7 , the stirrer 1 of figure 8 has six more outer stirrer blades 7, which additional outer stirrer blades 7 are all positioned so that they have a normal vector Q on the side of the tip 4 with a positive angular component. This stirrer 1 has no net pumping effect.
- the stirrer 1 shown in figure 9 has a different arrangement of inner stirrer blades 5 than the previously described stirrers 1. All four inner stirrer blades 5 are placed so that they have a normal vector N on the side of the tip 4 with a negative angular component, meaning that if the stirrer 1 is rotated in a positive angular direction ⁇ during use, the inner stirrer blade 5 will create an axial displacement of molten glass away from the tip 4.
- the outer stirrer blades 7,8 are arranged similarly to the outer stirrer blades 7, 8 of the stirrer of figure 8 , only their total number is eight, instead of twelve.
- the stirrer 1 shown in figure 10 only has a single set of two inner stirrer blades 5, both placed so that they have a normal vector N on the side of the tip 4 with a negative angular component, meaning that if the stirrer 1 is rotated in a positive angular direction ⁇ during use, the inner stirrer blade 5 will create an axial displacement of molten glass away from the tip 4.
- the outer stirrer blades 8 are arranged like the outer stirrer blades 8 of the stirrer of figure 7 , only their total number is four, instead of six.
- This stirrer 1 has a particularly strong pumping effect, so that it is mostly suitable for use in batch processing, although it may be used in continuous processes as well when there is a requirement for a pumping effect.
- the stirrer 1 shown in figure 11 has four inner stirrer blades 6 which are placed so that they have a normal vector P on the side of the tip 4 with a positive angular component, meaning that if the stirrer 1 is rotated in a positive angular direction ⁇ during use, the inner stirrer blade 5 will create an axial displacement of molten glass away towards the tip 4.
- the outer stirrer blades 8 are arranged in two groups of fours, which are both similar to the four outer stirrer blades 8 of the stirrer 1 of figure 1 that are placed away from the tip 4. These have a normal vector R on the side of the tip with a negative angular component, meaning that if the stirrer is rotated in a positive angular direction ⁇ during use, these outer stirrer blades 8 will create an axial displacement of molten glass away from the tip 4.
- rods 9 extend only in radial direction from the shaft 2 and are straight rods. It is of course also possible that the rods 9 additionally have an axial and/or angular direction and/or that they are curved.
- outer stirrer blades 7,8 each have a single normal vector. It is also possible that an outer stirrer blade has different blade sections with different normal vectors. It is also possible that an outer stirrer blade has several blade sections with a normal vectors with mutually different angular components.
- Such an outer stirrer blade could for instance be a combination of the outer stirrer blades identified by numbers 7 and 8 in figure 9 .
- This single outer stirrer blade would then be mounted on the shaft as in figure 9 but by executing the rod between outer stirrer blades 7 and 8 shorter than in figure 9 , so that this rod would support the single combined outer stirrer blade only on one side, the side facing the shaft 2.
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- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Engineering & Computer Science (AREA)
- Materials Engineering (AREA)
- Organic Chemistry (AREA)
- Mixers Of The Rotary Stirring Type (AREA)
Abstract
Stirrer (1) for stirring molten glass (16), whereby the stirrer (1) comprises
- a shaft (2) having a tip (4) and having a central longitudinal axis (L), and
- one or more inner stirrer blades (5,6) which are attached to the shaft (2), and
- one or more outer stirrer blades (7,8) which are attached to the shaft (2), whereby the inner stirrer blades (5,6) are attached closer to the shaft (2) than the outer stirrer blades (7,8),
whereby, when considering the stirrer in a cylindrical coordinate system (11), both the one or more inner stirrer blades (5,6) as well as the one or more outer stirrer blades (7,8) are disposed at an angle (α, β) to the central longitudinal axis (L), whereby said angle (α, β) is between 0° and 90° not including these values, and are disposed having a least a blade section with a normal vector (N, P, Q, R), on the side directed towards the tip (4), with an angular component (NA, PA, QA, RA).
- a shaft (2) having a tip (4) and having a central longitudinal axis (L), and
- one or more inner stirrer blades (5,6) which are attached to the shaft (2), and
- one or more outer stirrer blades (7,8) which are attached to the shaft (2), whereby the inner stirrer blades (5,6) are attached closer to the shaft (2) than the outer stirrer blades (7,8),
whereby, when considering the stirrer in a cylindrical coordinate system (11), both the one or more inner stirrer blades (5,6) as well as the one or more outer stirrer blades (7,8) are disposed at an angle (α, β) to the central longitudinal axis (L), whereby said angle (α, β) is between 0° and 90° not including these values, and are disposed having a least a blade section with a normal vector (N, P, Q, R), on the side directed towards the tip (4), with an angular component (NA, PA, QA, RA).
Description
- The invention concerns a stirrer for stirring molten glass, and apparatus for stirring molten glass which comprises such a stirrer and the use of such a stirrer for homogenizing molten glass.
- Molten glass needs to be homogenized before it can be used, especially in highly demanding applications. The reason for this is that the melt process of the constituents alone may leave inhomogeneities, which can present itself as discolorations or as sections with a different refractive index.
- Because of the high viscosity of molten glass, leading to a laminar flow and a near absence of mixing by diffusion, a stirring apparatus is necessary. Such a stirring apparatus essentially consists of a stirring chamber in which a stirrer is placed. Such stirring apparatuses may work in a continuous process, or may be batch apparatuses, treating one batch of molten glass at a time.
- Homogenization in molten glass relies on repeated elongation, chopping and redistribution of local inhomogeneities. It is therefore important to use a stirrer optimized to perform all these tasks.
- Such stirrers for molten glass are usually made of platinum or a platinum-based alloy, because this is the one of the few materials having sufficient mechanical strength and chemical inertness at the temperatures needed for melting glass. As the platinum price is very high, an important further consideration when designing stirrers for molten glass is to limit the amount of material needed.
- An alternative material that may be used, especially in less demanding glass stirring applications, is molybdenum or a molybdenum-based alloy, which may or may not be clad with platinum.
- Furthermore, due to the extreme conditions, especially the combination of temperature and viscosity, wear of the stirrer, leading to platinum loss and glass contamination, is also a significant consideration, requiring the speed of stirrer blades to be as low as possible.
- If a stirring apparatus is used in a continuous process, there is a further consideration that the stirrer should have no significant pumping function, as changes in the rotational speed will then cause changes in the pressure drop over the molten glass supply system, which will in turn create variations in the properties of glass products formed at the end of the molten glass supply system, eg sheets of display glass.
- Some examples of known stirrers for molten glass having no or only limited pumping effect are given in
DE102008017045 ,WO2011020625 andUS8434329 . Their stirrer blades are disposed parallel to the direction in which the stirrers are rotating or at right angles to this direction, meaning that either there is mainly cutting of stirrer blades through the molten glass leading to a chopping effect on inhomogeneities without much elongation of non-homogenous section and redistribution of inhomogeneities, or mainly horizontal movement of the molten glass and possible elongation of inhomogeneities, without significant chopping effect, so that the homogenization performance of these stirrers is not optimal. - In
US2009/0025428 a non-pumping stirrer is disclosed with stirrer blades disposed at an angle between 0° and 90°, so that vertical as well as a horizontal movement is imposed on the molten glass, leading to a much better homogenization. The non-pumping effect is obtained by giving the stirrer blades different angles so that, given a certain rotational direction, the pumping action is upward for some stirrer blades and downward for other stirrer blades. - This causes however several relatively small movement cycles in the stirring chamber, which is also not optimal for the homogenization performance.
- The present invention is intended to provide a solution to these and other disadvantages by providing a stirrer for stirring molten glass whereby the stirrer comprises:
- a shaft having a tip and having a central axis, and
- one or more inner stirrer blades which are attached to the shaft, and
- one or more outer stirrer blades which are attached to the shaft, whereby the inner stirrer blades are attached closer to the shaft than the outer stirrer blades,
- whereby, when considering the stirrer in a cylindrical coordinate system with the longitudinal axial coordinate of the cylindrical coordinate system defined to coincide with the central axis whereby the cylindrical coordinate system is further defined by a radial coordinate and an angular coordinate, both the one or more inner stirrer blades as well as the one or more outer stirrer blades are disposed at an angle to the central axis, whereby said angle is between 0° and 90° not including these values, and are disposed having a normal vector, on the side directed to the tip, with an angular component or are disposed having a blade section with a normal vector, on the side directed towards the tip, with an angular component.
- The angular component of the normal vector ensures that in use both a horizontal as well as a vertical force is exercised on the molten glass, leading to a good homogenization performance.
- For the avoidance of doubt, it is noted that attached can mean either directly attached, or indirectly attached by means of another structural element of the stirrer.
- Note that depending on the definition of the direction of increasing value of the longitudinal axial coordinate and the definition of the direction of increasing values of the angular coordinate, the specified angular component of the specified normal vector of a given stirrer blade may be considered to be positive or negative. This is not relevant for the definition of the invention as the direction of the stirrer blades in this invention is only considered in relation to each other.
- Due to the presence of inner and outer stirrer blades, more precise control of the movement of molten glass through the stirring chamber, and therefore more control over homogenization performance can be obtained by the designer of a stirrer.
- In particular for example a cycling movement such as in
US2009/0025428 can be avoided, so that a plug flow behavior of the molten glass through the mixes can be approximated. Of course, by appropriate placement of the inner and outer stirrer blades such cycling movement can also be enhanced if desired. - Further, a rapid mixing of molten glass from the inlet zone into the bulk of the molten glass in the stirred volume can be obtained, or avoided if so desired, thereby obtaining more or less mixing, as desired, with material having entered the stirring chamber earlier, so obtaining a good smoothing out of time-dependent composition variations.
- Also the pumping effect can be better controlled, to be either absent, or to be more constant over a range of rotational speeds, while maintaining a placement of the individual stirrer blades which is optimal for homogenization, thereby again increasing the options for a stirrer designer to obtain a desired performance depending on the detailed requirements of a particular homogenization task.
- In a preferred embodiment the one or more outer stirrer blades are mounted on rods or tubes extending at least partially in a radial direction from the shaft from the shaft, whereby the one or more outer stirrer blades each have two ends, whereby each of these ends is mounted on a different one of said rods or tubes, whereby the rods or tubes used for mounting the ends of an specific outer stirrer blade have a different angular position and/or axial position on the shaft.
- This way of mounting the outer stirrer blades, whereby they bridge the distance between two rods allows for relatively large stirrer blades to be used, thereby optimizing, compared to the known stirrers, the ratio of stirrer blade material, effective for homogenization and tube or rod material, which not effective for homogenization but is made of the same, equally expensive, material.
- For the avoidance of doubt it is mentioned that rods or tubes may have any cross-sectional shape, such as, but not limited to, round, square, elliptical.
- This allows the one or more outer stirrer blades to be executed as helically mounted blades or even as helicoidal blades.
- In another preferred embodiment the outer edge of at least one of the one or more outer stirrer blades is provided with a raised edge, whereby preferably all of the mentioned outer stirrer blades are provided with such an edge.
- This enhances the smearing effect of the stirrer, and thereby causes an improved elongation of inhomogeneities, one of the major factors for good homogenization.
- In another preferred embodiment the angular component of the normal vector of at least a blade section, in other words the entire blade or a part of a blade, of one or more of said inner and outer stirrer blades is negative and the angular component of the normal vector of at least a blade section of one or more of the inner and outer stirrer blades is positive.
- This ensures that in use at least one stirrer blade moves the molten glass up and at least one stirrer blade moves the molten glass down, so that a repeated passage of at least part of the molten glass through the stirred volume is ensured.
- In another preferred embodiment, the stirrer comprises two or more of said inner stirrer blades, whereby the angular component of the normal vector of at least one of said inner stirrer blades is negative and the angular component of the normal vector of at least one other of said inner stirrer blades is positive and whereby the number and size of said inner stirrer blades having a normal vector with a negative angular component is the same as the number and size of said inner stirrer blades having a normal vector with a positive angular component.
- This ensure that there is no net pumping effect from the inner stirrer blades.
- Similarly, to obtain a lack of pumping effect from the outer stirrer blades, in a preferred embodiment the one or more outer stirrer blades in totality comprise two or more blade sections, whereby the angular component of the normal vector of at least one of said blade sections is negative and the angular component of the normal vector of at least one other of said blade sections is positive and whereby the number and size of said blade sections having a normal vector with a negative angular component is the same as the number and size of said blade sections having a normal vector with a positive angular component.
- In yet another preferred embodiment at least a blade section of one of said one or more outer stirrer blades extends over a certain axial section of the stirrer, whereby at least one of said one or more inner stirrer blades is placed in the same axial section, whereby the signs of the angular components of the normal vectors of this inner stirrer blade and this blade section of the outer stirrer blade are opposite.
It should be noted that in a preferred embodiment the angular component of the normal vector of an outer or inner stirrer blade on the side directed towards the tip, can be a single value or can have only a single sign over the entire outer or inner stirrer blade. - In this case an inner or outer stirrer blade only has one single blade section, so that in this case the term blade section of an outer stirrer blade is equivalent to the outer stirrer blade and the term blade section of an inner stirrer blade is equivalent to the inner stirrer blade.
- The invention further concerns an apparatus for stirring molten glass comprising a stirring chamber and having a stirrer according to any one of the previous claims which is mounted in the stirring chamber whereby the stirrer is rotatable around the central axis of the stirrer.
- In order to explain the invention, any without limiting the invention in any way, examples of preferred embodiments are given below, referring to the following figures:
-
Figure 1 , showing a schematic view in perspective of a stirrer according to the invention; -
Figure 2 , showing a side view of the stirrer offigure 1 ; -
Figure 3 , showing a cross-section according to III-III of the stirrer of the previous figures; -
Figure 4 , showing a cross-section according to IV-IV of the stirrer of the previous figures; -
Figure 5 , showing a cross-section according to V-V of the stirrer of the previous figures; -
Figure 6 , showing the use of the stirrer of the previous figures; -
Figure 7 , showing a schematic view in perspective of another stirrer according to the invention; -
Figure 8 , showing a schematic view in perspective of yet another stirrer according to the invention; -
Figure 9 , showing a schematic view in perspective of yet another stirrer according to the invention; -
Figure 10 , showing a schematic view in perspective of yet another stirrer according to the invention; and -
Figure 11 , showing two side views, in directions which are mutually different by 90°, of yet another stirrer according to the invention. - The
stirrer 1 shown infigures 1 to 5 consists mainly of ashaft 2, which is provided at one extreme with aconnector 3 for connecting theshaft 2 to a drive, and nearer to the other extreme, further to be called thetip 4, with a number of stirrer blades. Theshaft 2 has a central longitudinal axis L which during use will be the axis of rotation of thestirrer 1. - The stirrer blades can be grouped in two groups, more specifically
inner stirrer blades shaft 2 and which are helicoidally shaped, meaning shaped like a part of a helicoid, andouter stirrer blades rods 9 which are attached to theshaft 2. - The
outer stirrer blades shaft 2 according to the intersection of a plane and a cylinder, and which have a raisededge 10 at their outermost edge. Theinner stirrer blades shaft 2 and theouter stirrer blades shaft 2. - In this embodiment, but not necessarily, the raised edged 10 is present both above as well as below the main body of the
outer stirrer blades edge 10 serves to reinforce theouter stirrer blades - The stirrer geometry will further be considered in a cylindrical coordinate system, similar to the cylindrical coordinate
system 11 drawn infigure 1 , but with the longitudinal axial coordinate z of the cylindrical coordinate system defined to coincide with the central axis L and having an increasing value from theconnector 3 to thetip 4, and further having a radial coordinate ρ and an angular coordinate φ, defined to have an increasing value in clockwise direction when looking from theconnector 3 to thetip 4. - There are four
inner stirrer blades inner stirrer blades - The two
inner stirrer blades 5 closest to the tip have a normal vector N on the side of thetip 4 with a negative angular component NA, so with a direction opposite to the defined direction of the angular coordinate φ, meaning that if thestirrer 2 is rotated in a positive angular direction φ during use, theseinner stirrer blades 5 will create an axial displacement of molten glass away from thetip 4. - The two
inner stirrer blades 6 furthest away from thetip 4 have a normal vector P on the side of thetip 4 with a positive angular component PA, so with a direction coinciding with the defined direction of the angular coordinate φ, meaning that if thestirrer 2 is rotated in a positive angular direction φ during use, theseinner stirrer blades 6 will create an axial displacement of molten glass towards thetip 4. - As all
inner stirrer blades inner stirrer blades - The
outer stirrer blades rods 9 which are attached to theshaft 2 at different angular and axial positions, more specifically at angular positions 90° apart, in line with theouter stirrer blades shaft 2. Eachouter stirrer blade different rod 9, and whereby somerods 9 are attached to the ends of twoouter stirrer blades other rods 9 are only a attached to the end of a singleouter stirrer blade - Note that in the present example the
outer blades rods 9. It is however also possible thatouter blades rods 9 at a point between the attachment point to theshaft 2 and the free end of therods 9. - The
outer stirrer blades shaft 2 as theinner stirrer blades - There are eight
outer stirrer blades - The four
outer stirrer blades 7 closest to thetip 4 have a normal vector Q on the side of thetip 4 with a positive angular component QA, meaning that if thestirrer 2 is rotated in a positive angular direction φ during use, theseouter stirrer blades 7 will create an axial displacement of molten glass towards thetip 4. - The four
outer stirrer blades 8 furthest away from thetip 4 have a normal vector R on the side of the tip with a negative angular component RA, meaning that if the stirrer is rotated in a positive angular direction φ during use, theseouter stirrer blades 8 will create an axial displacement of molten glass away from thetip 4. - As all
outer stirrer blades outer stirrer blades - The
shaft 2, inner andouter stirrer blades rods 9 are all made of dispersion-hardened platinum. - The use of the stirrer is simple and as follows, and as illustrated in
figure 6 . - It is placed, connected with its
connector 3 to adrive 12, in a stirringchamber 13, which is provided with aninlet 14 and outlet formolten glass 15. The stirrer diameter d is only slightly smaller than the chamber diameterD. Molten glass 16 is made to flow through the mixing chamber and the stirrer is rotated, as shown infigure 6 , in this example clockwise as indicated by arrow A when looking from thedrive 12 towards thetip 4. - Two cycling flows 17 of
molten glass 16 are now established, both going repeatedly through the volumes swept by thestirrer blades molten glass 16. In particular the raisededge 10 is believed to play an important role in smearing themolten glass 16 close to the wall of the stirringchamber 13, thereby elongating impurities, to be chopped later by other actions of thestirrer 1. - Only limited mixing between the two
flows 16 occurs at the vertical level in the stirringchamber 13 where they meet. No significant cycling flow is established between thestirrer 1 and the wall of the stirringchamber 13, due to the narrow gap between them. - Due to the overall flow of molten glass from the
inlet 14 to theoutlet 15, molten glass is forced slowly from the upper cycling flow to the lower cycling flow, and then to theoutlet 15. - Note that in possible variants, especially in batch processing of molten glass, the stirrer may be significantly smaller than the stirring chamber, which is in that case formed by the vessel in which the stirring is performed.
- In yet another variant the stirrer may be placed in a long channel through which glass flows, whereby the channel itself forms the stirring chamber.
- The alternative stirrers shown in
figures 7 to 11 differ from the stirrer shown infigure 1 by having a different number and different arrangement of inner and outer stirrer blades. - The
stirrer 1 shown infigure 7 has the same number and arrangement ofinner stirrer blades figure 1 . The arrangement ofouter stirrer blades 8 is different, in that this stirrer has sixouter stirrer blades 8, which are all positioned so that they have a normal vector R on the side of thetip 4 with a negative angular component. Thisstirrer 1 has a pumping effect, when rotated in a positive angular direction φ, away from thetip 4. This pumping effect is dependent on the rotational speed of thestirrer 1 so that thisstirrer 1 is mostly suitable for batch-wise processing of molten glass. - The
stirrer 1 shown infigure 8 has the same number and arrangement ofinner stirrer blades stirrer 1 offigures 1 and7 . The arrangement of outer stirrer blades is different, in that in addition to theouter stirrer blades 8 of thestirrer 1 offigure 7 , thestirrer 1 offigure 8 has six moreouter stirrer blades 7, which additionalouter stirrer blades 7 are all positioned so that they have a normal vector Q on the side of thetip 4 with a positive angular component. Thisstirrer 1 has no net pumping effect. - The
stirrer 1 shown infigure 9 has a different arrangement ofinner stirrer blades 5 than the previously describedstirrers 1. All fourinner stirrer blades 5 are placed so that they have a normal vector N on the side of thetip 4 with a negative angular component, meaning that if thestirrer 1 is rotated in a positive angular direction φ during use, theinner stirrer blade 5 will create an axial displacement of molten glass away from thetip 4. Theouter stirrer blades outer stirrer blades figure 8 , only their total number is eight, instead of twelve. - As the
outer stirrer blades inner stirrer blades 5 do, thisstirrer 1 has a net pumping effect. - The
stirrer 1 shown infigure 10 only has a single set of twoinner stirrer blades 5, both placed so that they have a normal vector N on the side of thetip 4 with a negative angular component, meaning that if thestirrer 1 is rotated in a positive angular direction φ during use, theinner stirrer blade 5 will create an axial displacement of molten glass away from thetip 4. Theouter stirrer blades 8 are arranged like theouter stirrer blades 8 of the stirrer offigure 7 , only their total number is four, instead of six. Thisstirrer 1 has a particularly strong pumping effect, so that it is mostly suitable for use in batch processing, although it may be used in continuous processes as well when there is a requirement for a pumping effect. - The
stirrer 1 shown infigure 11 has fourinner stirrer blades 6 which are placed so that they have a normal vector P on the side of thetip 4 with a positive angular component, meaning that if thestirrer 1 is rotated in a positive angular direction φ during use, theinner stirrer blade 5 will create an axial displacement of molten glass away towards thetip 4. - The
outer stirrer blades 8 are arranged in two groups of fours, which are both similar to the fourouter stirrer blades 8 of thestirrer 1 offigure 1 that are placed away from thetip 4. These have a normal vector R on the side of the tip with a negative angular component, meaning that if the stirrer is rotated in a positive angular direction φ during use, theseouter stirrer blades 8 will create an axial displacement of molten glass away from thetip 4. - For completeness it is noted that also the
connector 3 is executed differently. - It is noted that in the above examples the
rods 9 extend only in radial direction from theshaft 2 and are straight rods. It is of course also possible that therods 9 additionally have an axial and/or angular direction and/or that they are curved. - It is further noted that in the examples above the
outer stirrer blades
It is also possible that an outer stirrer blade has different blade sections with different normal vectors. It is also possible that an outer stirrer blade has several blade sections with a normal vectors with mutually different angular components. - Such an outer stirrer blade could for instance be a combination of the outer stirrer blades identified by
numbers figure 9 . - These two outer stirrer blades lie in the same plane, and could therefore easily be made as a single outer stirrer blade from a single straight sheet with a blade section corresponding to
outer stirrer blade 7 and a blade section corresponding toouter stirrer blade 8. - This single outer stirrer blade would then be mounted on the shaft as in
figure 9 but by executing the rod betweenouter stirrer blades figure 9 , so that this rod would support the single combined outer stirrer blade only on one side, the side facing theshaft 2.
Claims (15)
- Stirrer (1) for stirring molten glass (16), whereby the stirrer (1) comprises- a shaft (2) having a tip (4) and having a central longitudinal axis (L), and- one or more inner stirrer blades (5,6) which are attached to the shaft (2), and- one or more outer stirrer blades (7,8) which are attached to the shaft (2), whereby the inner stirrer blades (5,6) are attached closer to the shaft (2) than the outer stirrer blades (7,8),whereby, when considering the stirrer in a cylindrical coordinate system (11) with the longitudinal axial coordinate (z) of the cylindrical coordinate system (11) defined to coincide with the central longitudinal axis (L), whereby the cylindrical coordinate system (11) is further defined by a radial coordinate (p) and an angular coordinate (φ), both the one or more inner stirrer blades (5,6) as well as the one or more outer stirrer blades (7,8) are disposed at an angle (α, β) to the central longitudinal axis (L), whereby said angle (α, β) is between 0° and 90° not including these values, and are disposed having a least a blade section with a normal vector (N, P, Q, R), on the side directed towards the tip (4), with an angular component (NA, PA, QA, RA).
- Stirrer according to any one of the previous claims, characterized in that the one or more inner stirrer blades (5,6) are mounted against the shaft (2) and are preferably executed as helicoidal blades or a helicoidal blade.
- Stirrer according to any one of the previous claims, characterized in that the one or more outer stirrer blades (7,8) are mounted on rods (9) or tubes extending at least partially in a radial direction from the shaft (2).
- Stirrer according to claim 3, characterized in that the one or more outer stirrer blades (7,8) each have two ends, whereby each of these ends is mounted on a different one of said rods (9) or tubes, whereby the rods (9) or tubes used for mounting the ends of an specific outer stirrer blade (7,8) have a different angular position and/or axial position on the shaft (2).
- Stirrer according to claim 3 or 4, characterized in that the one or more outer stirrer blades (7,8) are each mounted on two or more of said rods (9) or tubes, whereby the rods (9) or tubes used for mounting an outer stirrer blade (7,8) are placed at angular positions on the shaft which are mutually different by at least 30° and which are preferably mutually different by 90°.
- Stirrer according to any one of claims 3 to 5, characterized in that the one or more outer stirrer (7,8) blades are placed following the line formed by the intersection of a cylinder and a plane making an angle with the central axis of that cylinder.
- Stirrer according to any one of claims 3 to 6, characterized in that the outer edge of at least one of the one or more outer stirrer blades (7,8) is provided with a raised edge (10), whereby preferably all of the mentioned outer stirrer blades (7,8) are provided with such a raised edge (10).
- Stirrer according to any one of the previous claims, characterized in that the angular component (NA, PA, QA, RA) of said normal vector (N, P, Q, R) of at least a blade section of one or more of said inner and outer stirrer blades (5, 6, 7, 8) is negative and the angular component (NA, PA, QA, RA) of said normal vector (N, P, Q, R) of at least a blade section of one or more of the inner and outer stirrer blades (5, 6, 7, 8) is positive.
- Stirrer according to claim 8, characterized in that it comprises two or more of said inner stirrer blades (5,6), whereby the angular component (NA, PA) of the normal vector (N, P) of at least one of said inner stirrer blades (5,6) is negative and the angular component (NA, PA) of the normal vector (N, P) of at least one other of said inner stirrer blades (5,6) is positive and whereby the number and size of said inner stirrer blades (5,6) having a normal vector (N, P) with a negative angular component (NA, PA) is the same as the number and size of said inner stirrer blades having a normal vector (N, P) with a positive angular component (NA, PA).
- Stirrer according to claim 8 or 9, characterized in that the one or more outer stirrer blades (7,8) in totality comprise two or more blade sections, whereby the angular component (QA, RA) of the normal vector (Q, R) of at least one of said blade sections is negative and the angular component (QA, RA) of the normal vector (Q, R) of at least one other of said blade sections is positive and whereby the number and size of said blade sections having a normal vector (Q, R) with a negative angular component (QA, RA) is the same as the number and size of said blade sections having a normal vector (Q, R) with a positive angular component (QA, RA).
- Stirrer according to any one of claims 8 to 10, characterized in that at least a blade section of one of said one or more outer stirrer blades (7,8) extends over a certain axial section of the shaft (1), whereby at least one of said one or more inner stirrer blades (7,8) is placed in the same axial section, whereby the signs of the angular components (NA, PA, QA, RA) of the normal vectors (N, P, Q, R) of this inner stirrer blade (5,6) and this blade section of the outer stirrer blade (7,8) are opposite.
- Stirrer according to any one of the previous claims, characterized in that most, and preferably all, of the mentioned one or more inner and outer stirrer blades (5,6,7,8) are disposed at an angle (α, β) to the central longitudinal axis (L) which is between 10° and 80° including said values, and which is preferably between 20° and 70° including said values.
- Stirrer according to any one of the previous claims, characterized in that the stirrer (1) is made of platinum or a platinum alloy or of molybdenum or a molybdenum-based alloy.
- An apparatus for stirring molten glass (16) comprising a stirring chamber (13) having a stirrer (1) according to any one of the previous claims which is mounted in the stirring chamber (13) whereby the stirrer (1) is rotatable around said central longitudinal axis (L).
- Use of a stirrer (1) according to any one of claims 1 to 13 for homogenizing molten glass (16).
Priority Applications (22)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
EP15156128.9A EP3059007A1 (en) | 2015-02-23 | 2015-02-23 | Stirrer for stirring molten glass, apparatus for stirring molten glass comprising such a stirrer and use of such a stirrer |
RU2016105978U RU168388U1 (en) | 2015-02-23 | 2016-02-20 | Device for mixing molten glass |
TW105202462U TWM537588U (en) | 2015-02-23 | 2016-02-22 | Device for stirring molten glass, apparatus for stirring molten glass comprising such a device and use of such a device |
US15/552,589 US10676385B2 (en) | 2015-02-23 | 2016-02-22 | Device for stirring molten gas |
ES201630215U ES1157008Y (en) | 2015-02-23 | 2016-02-22 | DEVICE FOR SHAKING FUNDED GLASS, APPARATUS FOR SHAKING CASTED GLASS THAT INCLUDES SUCH DEVICE AND USE OF SUCH DEVICE |
FR1651407A FR3032957B3 (en) | 2015-02-23 | 2016-02-22 | MOLTEN GLASS STIRRING DEVICE, MOLTEN GLASS STIRRING APPARATUS COMPRISING SUCH DEVICE AND USE OF SUCH A DEVICE |
EP16706575.4A EP3261756B1 (en) | 2015-02-23 | 2016-02-22 | Stirrer for stirring molten glass |
CN201680011419.4A CN107249724B (en) | 2015-02-23 | 2016-02-22 | Apparatus for stirring molten glass |
CZ2016-32131U CZ30172U1 (en) | 2015-02-23 | 2016-02-22 | Device to agitate melted glass and apparatus for agitating melted glass comprising such device |
TW105105117A TW201638028A (en) | 2015-02-23 | 2016-02-22 | Device for stirring molten glass, apparatus for stirring molten glass comprising such a device and use of such a device |
PCT/EP2016/053642 WO2016135084A1 (en) | 2015-02-23 | 2016-02-22 | Device for stirring molten glass |
BR202016003925-3U BR202016003925Y1 (en) | 2015-02-23 | 2016-02-23 | SHAKER TO SHAKE CAST GLASS |
CN201620136492.1U CN205893055U (en) | 2015-02-23 | 2016-02-23 | A plunger for stirring molten glass's agitator reaches including this type of agitator |
KR2020160000961U KR200492911Y1 (en) | 2015-02-23 | 2016-02-23 | Device for stirring molten glass, apparatus for stirring molten glass comprising such a device and use of such a device |
ATGM50035/2016U AT15242U1 (en) | 2015-02-23 | 2016-02-23 | Apparatus for stirring molten glass, apparatus for stirring molten glass comprising such apparatus and the use of such apparatus |
DE202016100936.7U DE202016100936U1 (en) | 2015-02-23 | 2016-02-23 | Apparatus for stirring molten glass, apparatus for stirring molten glass comprising such apparatus |
JP2016001711U JP3206061U (en) | 2015-02-23 | 2016-04-13 | Device for stirring molten glass, apparatus for stirring molten glass including such device, and use of such device |
US29/572,349 USD800808S1 (en) | 2015-02-23 | 2016-07-27 | Stirrer |
US29/572,347 USD800807S1 (en) | 2015-02-23 | 2016-07-27 | Stirrer |
US29/572,350 USD849070S1 (en) | 2015-02-23 | 2016-07-27 | Stirrer |
RU2016147319U RU170436U1 (en) | 2015-02-23 | 2016-12-02 | A device for mixing molten glass, an apparatus for mixing molten glass containing such a device, and the use of such a device |
US29/638,084 USD918279S1 (en) | 2015-02-23 | 2018-02-23 | Stirrer |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
EP15156128.9A EP3059007A1 (en) | 2015-02-23 | 2015-02-23 | Stirrer for stirring molten glass, apparatus for stirring molten glass comprising such a stirrer and use of such a stirrer |
Publications (1)
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EP3059007A1 true EP3059007A1 (en) | 2016-08-24 |
Family
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EP15156128.9A Withdrawn EP3059007A1 (en) | 2015-02-23 | 2015-02-23 | Stirrer for stirring molten glass, apparatus for stirring molten glass comprising such a stirrer and use of such a stirrer |
EP16706575.4A Active EP3261756B1 (en) | 2015-02-23 | 2016-02-22 | Stirrer for stirring molten glass |
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EP16706575.4A Active EP3261756B1 (en) | 2015-02-23 | 2016-02-22 | Stirrer for stirring molten glass |
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US (5) | US10676385B2 (en) |
EP (2) | EP3059007A1 (en) |
JP (1) | JP3206061U (en) |
KR (1) | KR200492911Y1 (en) |
CN (2) | CN107249724B (en) |
AT (1) | AT15242U1 (en) |
BR (1) | BR202016003925Y1 (en) |
CZ (1) | CZ30172U1 (en) |
DE (1) | DE202016100936U1 (en) |
ES (1) | ES1157008Y (en) |
FR (1) | FR3032957B3 (en) |
RU (2) | RU168388U1 (en) |
TW (2) | TWM537588U (en) |
WO (1) | WO2016135084A1 (en) |
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CN109803932A (en) * | 2016-12-22 | 2019-05-24 | 日本电气硝子株式会社 | The manufacturing method of blender and glass plate |
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EP3059007A1 (en) * | 2015-02-23 | 2016-08-24 | Umicore AG & Co. KG | Stirrer for stirring molten glass, apparatus for stirring molten glass comprising such a stirrer and use of such a stirrer |
WO2017169333A1 (en) * | 2016-03-29 | 2017-10-05 | 日本電気硝子株式会社 | Molten glass stirring device and method for manufacturing glass article |
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CN109803932A (en) * | 2016-12-22 | 2019-05-24 | 日本电气硝子株式会社 | The manufacturing method of blender and glass plate |
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Also Published As
Publication number | Publication date |
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CZ30172U1 (en) | 2016-12-20 |
RU170436U1 (en) | 2017-04-25 |
CN107249724A (en) | 2017-10-13 |
CN205893055U (en) | 2017-01-18 |
JP3206061U (en) | 2016-09-01 |
USD849070S1 (en) | 2019-05-21 |
FR3032957A3 (en) | 2016-08-26 |
EP3261756B1 (en) | 2021-05-26 |
BR202016003925Y1 (en) | 2021-11-09 |
EP3261756A1 (en) | 2018-01-03 |
ES1157008Y (en) | 2016-10-10 |
USD800807S1 (en) | 2017-10-24 |
RU168388U1 (en) | 2017-02-01 |
WO2016135084A9 (en) | 2017-07-06 |
BR202016003925U2 (en) | 2016-08-30 |
FR3032957B3 (en) | 2017-03-24 |
ES1157008U (en) | 2016-07-18 |
USD918279S1 (en) | 2021-05-04 |
TW201638028A (en) | 2016-11-01 |
KR200492911Y1 (en) | 2020-12-31 |
USD800808S1 (en) | 2017-10-24 |
CN107249724B (en) | 2021-07-27 |
WO2016135084A1 (en) | 2016-09-01 |
DE202016100936U1 (en) | 2016-04-05 |
TWM537588U (en) | 2017-03-01 |
AT15242U1 (en) | 2017-04-15 |
US20180334404A1 (en) | 2018-11-22 |
KR20160003000U (en) | 2016-08-31 |
US10676385B2 (en) | 2020-06-09 |
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